EP0462687B1

EP0462687B1 - High capacity vane

Info

Publication number: EP0462687B1
Application number: EP91250161A
Authority: EP
Inventors: Kenneth J. Fewel, Jr.
Original assignee: Peerless Manufacturing Co
Current assignee: Peerless Manufacturing Co
Priority date: 1990-06-20
Filing date: 1991-06-18
Publication date: 1996-03-20
Anticipated expiration: 2011-06-18
Also published as: US5104431A; EP0462687A1; JPH0731816A; DE69118023T2; DE69118023D1; ES2084096T3; JP3223322B2

Description

TECHNICAL FIELD

This invention relates to a vane, particularly a vane for liquid-gas separation, such as condensate from vapors, seawater from air, and absorptive liquids from treated gases.

BACKGROUND OF THE INVENTION

Virtually all internal combustion engines require the use of an air filtering mechanism to maintain the inlet air flowing into the engine as free of contaminants and as clean as possible to maximize the service life of the engine. This requirement is particularly important when the engines are mounted on shipboard and the available air is salt and moisture laden. In such an environment, one of the primary requirements of such separators is to separate the moisture from the air. This is particularly important when the marine engines are gas turbines, where moisture droplets impinging on the blades of the turbines can do severe damage.
As can readily be understood, space aboard a ship for such separators is often at a premium, however, the separators must perform their function adequately in order to prevent damage to the engine. Therefore, there is an ongoing need to increase the efficiency and the compactness of these separators.
There is an ever increasing demand for air filtering mechanisms which have increased air flow velocities while maintaining adequate cleaning capability, a minimization of the pressure drop across the filter, representing the energy required to pass the air through the filter, and the size of the filter itself. These requirements are particularly important when the engines are mounted on shipboard and the available air for combustion which must travel through the filtering mechanism is moisture and salt laden. US-A-3,912,471 discloses a high velocity eliminator which does not have pockets, but merely hooks. DE-A-16 19 839 discloses a device with only single pockets for each turn of the vane. The P8X vane manufactured by Peerless Manufacturing Company also only has one pocket per turn of the vane. DE-C-615 363 discloses a continuously curved device which does not have alternately turning vanes.
The development of the present invention fulfills a need for enhanced flow velocities while achieving excellent characteristics for contaminant separation pressure drop and filter size.

SUMMARY OF THE INVENTION

This invention relates to a high capacity vane for a moisture separator to separate moisture from air flowing in an air flow direction, the vane having a first member extending at a predetermined angle relative to the direction of air flow from a leading edge to a trailing edge and a second member extending from the trailing edge of the first member at a second predetermined angle relative to the direction of air flow, characterized in that the first member and the second member each have at least one upstream cavity formed therein and at least one downstream cavity formed therein, a first side of the first member having first and second longitudinal slots formed therein perpendicular the direction of air flow, each of said slots providing an opening into one of said cavities, a second side of said second member having first and second slots formed therein extending perpendicular the direction of air flow, each of said slots opening into a cavity in said second member. The said first side of the first member and said second side of the second member being on opposite sides of said vane.

BRIEF DESCRIPTION OF THE DRAWINGS

For a more complete understanding of the present invention and the advantages thereof, reference is now made to the following description taken in conjunction with the accompanying drawings, in which:

FIGURE 1 is a perspective view of a separator assembled of vanes forming a first embodiment of the present invention;
FIGURE 2 is a horizontal cross sectional view of a vane forming a first embodiment of the present invention;
FIGURE 3 is a horizontal cross sectional view of a vane forming a second embodiment of the present invention;
FIGURE 4 is a horizontal cross sectional view of a steel vane forming a second embodiment of the present invention;
FIGURE 5 is a horizontal cross sectional view of the components forming the vane of FIGURE 4;
FIGURE 6 is a side view of one of the components of the vane of FIGURE 4 illustrating the formation of the slots;
FIGURE 7 is a horizontal cross sectional view of a steel vane forming a third embodiment of the present invention;
FIGURE 8 is a graph showing a performance comparison between a vane of the present invention and prior known vanes;
FIGURE 9 is a chart which compares liquid capacity between vanes of the present invention and prior known vane design; and
FIGURES 10 and 11 are charts comparing particle size efficiency between vanes of the present invention and a prior known vane for different flow velocities.

DETAILED DESCRIPTION

With reference now to the drawings, wherein like reference characters designate like or similar parts throughout the several views, FIGURE 1 illustrates broadly a separator 10 formed of an assembly of vanes 12 for the separation of moisture from an air flow passing through the separator 10 in the direction of arrow 14.
As will be understood, the vanes 12 are extremely high performance vanes relative to that previously in existence, which permits the separator 10 to be made more compact for a given performance requirement.
With reference to FIGURE 2, the construction of vanes 12 will be described. Preferably, vanes 12 are formed of an aluminum extrusion which define a series of boxlike members 16 and 18 which extend generally along the direction of air flow but at a predetermined angle relative thereto. Each of the members is hollow and defines an upstream cavity 20 and a downstream cavity 22 which extends the entire height of the vanes. A longitudinal upstream opening or slot 24 extends through a first side 26 of member 16 into the upstream cavity 20. A similar slot 28 opens into the downstream cavity 22.
A second side 30 of member 18, on a side opposite that of the first side 26, includes similar slots 24 and 28 opening into cavities 20 and 22 respectively.
As can be seen in FIGURE 2, as air laden with moisture flows in the direction of arrow 14, some of the air will enter the cavities 20 and 22 of member 16, where the convoluted and multi-directional airflow which results separates out the denser moisture and drains the separated moisture along the cavities to the bottom of the separator. Similarly, air flow passing the first member will impinge upon the similar slots in the member 18 of the adjacent vane, which will further agitate the air flow for moisture separation.
It will be understood that the vane of the present invention can be utilized for all forms of liquid and gas separation. Separation of moisture from air is simply one example of this use. For example, the vanes can also be used to remove condensate from vapors and absorptive liquid from treated gases.
It can be seen that each cavity 20 and 22 has a transverse thickness or depth D which generally is perpendicular to the direction of air flow. Preferably, this dimension D is less than 1/45 of the vane wavelength W₁ and less than 1/14 of the peak-to-peak amplitude A of the vane while still providing drainage space amounting to greater than 50 percent of the vane cross sectional area. However, the dimension D should not be too small so as to create surface tension concerns for draining separated fluids along the cavities.
The drainage space referred to is effectively the volume of each cavity 20 and 22, divided by the height H. This volume is defined by the length L of each cavity, which generally lies parallel the direction of air flow, the depth D and the height H of the vane [see FIGURE 6]. The vane cross sectional area would be the width W of the vane times the thickness DV of the vane.
These relationships allow an increase in the speed of the air flow through the vanes without re-entrainment of separated fluids, thus increasing the capacity of the vanes 12 over prior known designs. For example, vanes constructed in accordance with the designs of the present invention are capable of air flows of 19.81 m/s (65 ft/sec) without significant re-entrainment of separated fluids, while prior designs can only tolerate speeds of 13.72 m/s (45 ft/sec) before significant re-entrainment begins to occur.
With such a construction, vanes 12 will provide for a contraction of the flow necessary to pass through the vane of less than 33 percent, while still maintaining adequate tortuosity to separate droplets as small as ten micrometers (microns) in diameter with 95 percent efficiency
With reference now to FIGURE 3, a vane 40 forming a second embodiment of the present invention is illustrated. In vane 40 will be used a series of members 16, 18, 42 and 44. The construction of members 42 and 44 is identical to that of members 16 and 18, and vane 40 could be used in environments with very high moisture removal requirements.
With reference now to FIGURES 4-6, a vane 100 forming a third embodiment of the present invention is illustrated. As best seen in FIGURE 5, the vane 100 is formed by joining a first member 102 and a second member 104 to form each vane. Members 102 and 104 are preferably of carbon steel which are welded together at spacers 106 to define upstream cavities 20 and downstream cavities 22. As best seen in FIGURE 6 slots 24 are formed in alternating panels 108 of each member with the intervening panel 110 being solid. The slot opening into the upstream cavity 20 is preferably formed of a pair of equal length slots 112. The openings into the downstream cavity 22 are preferably formed of an intermediate slot 114 and shorter equal length outer slots 116.
In one separator constructed of vanes 100 in accordance with the teachings of the present invention, the members 102 and 104 were essentially identical in dimensional characteristics with the angle theta between each panel being 120°. The dimension X of each panel was 1.46 inches while the dimension Y was about 6.3 cm (2.48 inches). The height H, of the vane was about 101.6 cm (40 inches). The slots 112, 114, and 116 were each approximately 0.64 cm (1/4 inch) wide (dimension WS). The slots 112 were about 49.2 cm (19.38 inches) tall (dimension T1), the slot 114 was about 36.8 cm (14.5 inches) tall (dimension T2) and the slots 116 were about 30.5 cm (12 inches) tall (dimension T3). 1.3 cm (1/2 inch) separated the outer slots 112 and 116 from the upper and lower edges of the members while each slot was separated from its adjacent slot by 0.64 cm (a quarter inch).
With reference now to FIGURE 7, a vane 150 forming a fourth embodiment of the present invention is illustrated. Each vane 150 is formed of a first member 152 and a second member 154, with the members' spot welded together. Again, vanes 150 are preferably formed of steel. In the members 152 and 154, alternating panels 156 have u-shaped ridges 158 stamped therein which abut against panels 160 to define the upstream and downstream cavities 20 and 22. Slots 24 are then formed through the panels 160 as illustrated in a manner similar to vanes 100.
Vanes 40, 100 and 150 are all constructed as vane 12 in having the transverse thickness D of the drainage pocket less than 1/45 of the vane wavelength and less than 1/14 of the peak-to-peak amplitude, while still providing drainage space amounting to greater than 50 percent of the vane cross sectional area.
FIGURES 8-11 illustrate the significant enhanced performance characteristics for vanes as disclosed in the present invention as compared to a prior known high performance vane. These figures clearly show the advantage of the present invention. For the purposes of conversion to S.I. units, 1 inch W.C is equal to 249.1 Pa, 10 ft/sec is equal to 3.1 m/s, and 1 GPM/ft of width is equal to 14.9 Litres PM/metre of width.

Claims

A high capacity vane (12, 40, 100, 150) for a moisture separator (10) to separate moisture from air flowing in an air flow direction (14), the vane having a first member (16) extending at a predetermined angle relative to the direction of air flow from a leading edge to a trailing edge and a second member (18) extending from the trailing edge of the first member (16) at a second predetermined angle relative to the direction of air flow, characterized in that the first member (16) and the second member (18) each have at least one upstream cavity (20) formed therein and at least one downstream cavity (22) formed therein, a first side (26) of the first member having first and second longitudinal slots (24, 28) formed therein perpendicular the direction of air flow, each of said slots (24, 28) providing an opening into one of said cavities (20, 22), a second side (30) of said second member (18) having first and second slots (24, 28) formed therein extending perpendicular the direction of air flow, each of said slots (24, 28) opening into a cavity (20, 22) in said second member (18), the said first side (26) of the first member (16) and said second side (30) of the second member (18) being on opposite sides of said vane (12, 40, 100, 150).
The high capacity vane (12, 40, 100, 150) of Claim 1 wherein the high capacity vane is designed to be positioned relative to another high capacity vane of the same design at predetermined separations along a direction perpendicular the direction of air flow (14) to separate moisture from the air flow to form the moisture separator (10).
The high capacity vane (12, 40, 100, 150) of Claim 2 wherein the available cross-sectional area for flow between the vanes is reduced by less than 33% relative to the upstream flow cross-sectional area, while still maintaining adequate tortuosity to separate droplets as small as ten micrometers in diameter with 95% efficiency.
The high capacity vane (12, 40, 100, 150) of Claim 1 having a vane wave length (W) defined as the distance in the flow direction between repeating features of the vane, such as bends, and a peak-to-peak amplitude (A), defined as the distance between repeating features of the vanes in a direction perpendicular to the flow direction, said upstream and downstream cavities (20, 22) each having a transverse thickness (D), the transverse thickness of the cavities being less than 1/45 of the vane wave length (W) and less than 1/14 of the peak-to-peak amplitude (A).